Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
Recovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the...
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doaj-3e75ca0083034212857ee35f82805be22020-11-24T21:51:47ZengMDPI AGMinerals2075-163X2016-10-016410910.3390/min6040109min6040109Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching ProcessMingming Yu0Shuya Pang1Guangjun Mei2Xiaodong Chen3School of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaRecovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the majority of the impurities in the solution can be removed by adjusting the pH to 4.5 using a Na2S and NH3·H2O solution. Thirdly, the rare earths can be precipitated afterwards by adding a H2C2O4 solution and adjusting the pH to 2.0. Then rare earth oxides (REOs) can be obtained after calcining at 800 °C for 1 h. The characterization study of the waste phosphors and the rare earth oxide products was performed by XRD, XRF, and SEM-EDS analysis to determine the phase and morphological features. Influences of the factors, such as roasting temperatures and time, the addition of ammonium chloride on the roasting of waste phosphors, as well as the pH and the amount of oxalates on the precipitation of Y and Eu, were investigated. The maximum grade (99.84%) of mixed rare earth oxides and recovery rate (87.35%) of Y and Eu were obtained at the optimized conditions.http://www.mdpi.com/2075-163X/6/4/109waste phosphorschlorination roastingwater leachingrare earth elementsrecycling |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Mingming Yu Shuya Pang Guangjun Mei Xiaodong Chen |
spellingShingle |
Mingming Yu Shuya Pang Guangjun Mei Xiaodong Chen Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process Minerals waste phosphors chlorination roasting water leaching rare earth elements recycling |
author_facet |
Mingming Yu Shuya Pang Guangjun Mei Xiaodong Chen |
author_sort |
Mingming Yu |
title |
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process |
title_short |
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process |
title_full |
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process |
title_fullStr |
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process |
title_full_unstemmed |
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process |
title_sort |
recovering y and eu from waste phosphors using chlorination roasting—water leaching process |
publisher |
MDPI AG |
series |
Minerals |
issn |
2075-163X |
publishDate |
2016-10-01 |
description |
Recovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the majority of the impurities in the solution can be removed by adjusting the pH to 4.5 using a Na2S and NH3·H2O solution. Thirdly, the rare earths can be precipitated afterwards by adding a H2C2O4 solution and adjusting the pH to 2.0. Then rare earth oxides (REOs) can be obtained after calcining at 800 °C for 1 h. The characterization study of the waste phosphors and the rare earth oxide products was performed by XRD, XRF, and SEM-EDS analysis to determine the phase and morphological features. Influences of the factors, such as roasting temperatures and time, the addition of ammonium chloride on the roasting of waste phosphors, as well as the pH and the amount of oxalates on the precipitation of Y and Eu, were investigated. The maximum grade (99.84%) of mixed rare earth oxides and recovery rate (87.35%) of Y and Eu were obtained at the optimized conditions. |
topic |
waste phosphors chlorination roasting water leaching rare earth elements recycling |
url |
http://www.mdpi.com/2075-163X/6/4/109 |
work_keys_str_mv |
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